Les performances et la durabilité d’une pile à combustible à membrane échangeuse de proton (PEMFC) sont directement liées à la répartition de l’eau dans l’assemblage membrane-électrode (AME), plus particulièrement dans la membrane électrolyte. L’optimisation de cette répartition de l’eau, homogène et suffisante, est donc indispensable pour obtenir de bonnes performances et une grande durabilité. La répartition de l’eau dépend d’une part des conditions de fonctionnement et d’autre part de la géométrie des canaux de distribution des gaz dans les plaques mono ou bipolaires. Cependant, l’effet de ces paramètres n’est pas encore entièrement élucidé malgré de nombreuses études réalisées.Dans ce contexte, la première partie de cette thèse se focalise sur l’effet des conditions d’humidification des gaz et de température de fonctionnement sur les performances et la distribution de l’eau dans une pile de configuration en serpentin. Les profils d’eau à travers l’épaisseur de la membrane au centre de la surface active sont enregistrés par spectroscopie Raman operando. Le lien entre la distribution de l’eau et les performances de la pile sera discuté. Dans la deuxième partie, les performances et la distribution de l’eau dans une pile de configuration en parallèle sont étudiées aux mêmes conditions de température appliquées pour la pile de configuration en serpentin. Les résultats obtenus nous permettent de comparer directement les comportements de ces deux configurations. L’origine des différences de leur répartition de l’eau et donc de leurs performances sera clarifiée. Dans la troisième partie, nous nous concentrons sur la répartition de l’eau dans le plan d’une pile en serpentin aux différentes température de fonctionnement. La pile est alimentée en contre-flux. Les profils d’eau dans l’épaisseur de la membrane sont enregistrés pour trois zones : entrée, centre et sortie. Nous traçons par la suite la répartition de l’eau sur les interfaces cathodique et anodique. Ces informations nous apportent une meilleure compréhension de la répartition de l’eau dans cette configuration ainsi que l’effet du mode d’alimentation des gaz en contre-flux. / In a proton exchange membrane fuel cell (PEMFC), the performance and the durability of the system is directly related to the water management in the membrane electrode assembly (AME), particularly in the membrane electrolyte. The optimization of the water repartition, homogeneous and sufficient, is therefore essential to obtain good performance and great durability. The water management in the membrane depends both on the operating conditions and the gas flow-field design. However, the effect of these parameters is not yet fully understood despite numerous studies.In this context, the first part of this thesis focuses on the influence of gas humidification and operating temperature conditions on the performance and the water distribution in a serpentine flow-field cell. The inner water profiles across the membrane thickness at the center of the active surface are recorded by Raman spectroscopy operando. The relationship between the water distribution and the performance of the cell will be discussed. In the second part, the performance and the water distribution in a parallel flow-field cell are studied under the same temperature conditions applied for the serpentine flow-field cell. The results obtained allow us to directly compare the behavior of these two configurations. The origin of their water distribution and performance differences will be discussed. In the third part, we focus on the distribution of water in the plane of a serpentine flow-field cell at different operating temperatures. The cell is powered in counter-flow. The inner water profiles in the membrane are recorded for three zones: inlet, center and outlet. We then trace the water repartition on the cathodic and anodic interfaces. This information gives us a better understanding of the counter-flow effect on the water distribution in the plane of the serpentine flow-field cell.

L'état d'hydratation des électrolytes polymères pour piles à combustibles de type PEMFC et donc, la conductivité protonique de ce type d'électrolytes, est le point crucial pour comprendre et expliquer les performances électrochimiques de ce type de système. Le fonctionnement de la pile (création, absorption, diffusion, migration et désorption d'eau) conduit à une forte hétérogénéité de l'état d'hydratation du matériau polymère et donc de sa conductivité.La conductivité protonique des membranes actuellement utilisées comme électrolyte est le fait de la structure du matériau, des mécanismes de diffusion de l'eau et du proton, et des interactions eau-polymère au sein de la membrane. Nous nous sommes intéressés à ces problèmes et avons étudié les mécanismes d'hydratation et de diffusion par les techniques de spectroscopies vibrationnelles Infra-Rouge et Raman.Ce travail démontrera, entre autres, l'apport particulièrement intéressant des spectroscopies vibrationnelles in-situ pour la résolution de la problématique de la distribution de l'eau au sein de la membrane et son influence sur les performances de la pile. Nous proposons ici une étude de deux polymères perfluorosulfonés, le Nafion et l'Aquivion.Les propriétés d'absorption d'eau, de diffusion d'eau et de transport du proton dans ces deux membranes sont étudiées dans diverses conditions d'hydratation : dans les conditions d'équilibre, sous gradient d'activité chimique de l'eau (mesure in situ) et sous l'effet d'un champ électrique (mesure in situ et operando dans une pile en fonctionnement). La spectroscopie Infra-Rouge est utilisée pour étudier les changements structuraux des polymères ainsi que l'état de confinement de l'eau au cours de l'hydratation des membranes soumises à différentes valeurs de pression partielle d'eau et de température. Elle permet également d'étudier les interactions entre l'eau et les différents groupements chimiques présents dans la structure du polymère. L'ensemble des résultats est utilisé pour proposer des mécanismes d'absorption de l'eau ainsi que de dissociation des groupements acides de la membrane. La micro-spectroscopie Raman confocale, grâce à sa résolution spatiale micrométrique, permet de sonder l'épaisseur de la membrane et de déterminer le gradient d'eau transverse. Une cellule micro-fluidique a été développée pour l'étude des phénomènes de transport diffusif. Cette technique est actuellement la seule permettant de calculer les coefficients de diffusion équivalente à partir des gradients de concentration d'eau interne.Une pile à combustible spécialement adaptée aux mesures Raman, nous a permis, pour la première fois avec cette technique, de déterminer la distribution de l'eau à travers l'épaisseur de la membrane dans le système électrochimique en fonctionnement. Les informations ainsi obtenues sont des données primordiales pour comprendre, expliquer et prévoir l'impact de la distribution de l'eau au sein du cœur de pile sur les performances globales de ce système. / The water content of polymer electrolytes for Proton Exchange Membrane Fuel Cells and, thus, their proton conductivity, is the key issue to understand and to explain the electrochemical performances of the PEMFC electrochemical device. The fuel cell operation (creation, absorption, diffusion, migration and desorption of water) leads the hydration state of the membrane strongly heterogeneous. The proton conductivity of state-of-art polymer electrolytes results from the material structure, the water and proton diffusion mechanisms and the interactions between water and the polymer phase within the membrane. This work deals with these issues and uses vibrational spectroscopy techniques (Infra-Red and Raman) to study hydration and diffusion phenomena. Among others, this work shows the contribution of in-situ vibrational spectroscopies to the understanding of the water management issue and relationships between the water distribution throughout the membrane and the fuel cell electrochemical performances. Two perfluorosulfonated polymers, Nafion and Aquivion, are investigated.The water absorption and diffusion properties of these two membranes are studied under several hydration conditions: at the equilibrium, under external gradient of the water chemical activity and under the effect of an electric gradient (in-situ and operando measurements with the working fuel cell).Infrared spectroscopy is used to study structural modifications of the polymer phase occurring during the hydration process as well as the confinement state of water sorbed within the membrane. The last is submitted to different water vapor pressures and temperatures. This spectroscopy also allows to study interactions between water and the different chemical groups belonging to the polymer structure. Results are used to describe water absorption as well as the proton dissociation mechanism involving the sulfonic groups.Confocal Raman Micro-spectroscopy allows, by the spatial resolution at the micrometric scale, to probe the thickness of the membrane and to measure the inner, through-plane, water gradient. A micro-fluidic cell has been developed for the study of diffusion transport phenomena. This method is currently the only one by which equivalent diffusion coefficients can be calculated from internal water concentration gradients.A fuel cell especially designed for Raman measurements allowed us, for the first time by means of this technique, to determine the water distribution through the thickness of the membrane working in the electrochemical device. The new insights so obtained are essential for understanding, explaining and predicting the effects of the heterogeneous water distribution throughout the fuel cell heart on the electrochemical behavior.

Ces travaux de thèse portent sur l'optimisation des méthodes de fabrication des assemblages membrane électrodes des Piles à Membrane Echangeuse de Protons (PEMFC, Proton Exchange Membrane Fuel Cell). Ils ont pour objectif d'optimiser le dépôt des couches catalytiques sur la membrane par une méthode de transfert. Le procédé a été utilisé pour fabriquer d'une part des assemblages à membrane Nafion® pour les piles à combustible à membrane fonctionnant à 80 °C (PEMFC) et d'autre part des assemblages à membrane polybenzimidazole dopée en acide phosphorique pour les PEMFC à haute température (160 °C). Au cours de cette étude, la détermination précise de la quantité de platine a été rendue possible par des mesures non destructives en fluorescence X. Nous avons développé également une méthode originale de fabrication de suspensions de blendes Nafion-PBI qui ont été incorporées dans les électrodes des assemblages à membrane PBI. L'effet de la composition, des épaisseurs et du mode de préparation des électrodes sur les performances des assemblages a été discuté. Les assemblages membrane électrodes à membrane PBI ont été caractérisés par des mesures en polarisation et en spectroscopie d'impédance (EIS). La détermination de surface active d'électrode a été réalisée par des mesures en voltammétrie cyclique in-situ (CV). La mise au point du procédé de fabrication des électrodes par transfert de couches actives sur membrane a permis d'obtenir des informations importantes sur les conditions de préparation des électrodes. Les performances des assemblages à membrane Nafion® sont supérieures à celles obtenues sur des assemblages de référence avec des électrodes supportées sur couche de diffusion (GDE). Il a été possible de réaliser pour la première fois des assemblages avec un dépôt sur des membranes polybenzimidazole déjà dopées en acide, les premiers résultats obtenus sont extrêmement encourageants. Le procédé de transfert des couches catalytiques pourrait être adapté pour réaliser des dépôts sur d'autres variétés de membranes dopées ou non dopées en acide. / This work concerns the optimization of the fabrication processes of membrane electrode assemblies for the Proton Exchange Membrane Fuel Cell (PEMFC). The objective is to carry out the deposition of catalyst layers onto the membranes by a transfer process. The optimization of the catalyst layer compositions and its morphology is crucial for this process. Assemblies with Nafion® membranes for PEMFC working at 80 °C and phosphoric acid doped polybenzimidazole membranes for HTPEMFC (160 °C) have been prepared by this method. X-ray fluorescence spectrometry, due to its non destructive nature, was applied for precise analysis of platinum loading on the electrodes. In this work, a new method was also developed for the preparation of Nafion-PBI blend suspensions that have been incorporated in the electrodes of the PBI membrane electrodes assemblies. The PBI membrane electrode assemblies have been characterized by polarization measurements and electrochemical impedance spectroscopy (EIS). The in situ PEM Fuel Cell electrochemical surface area (ECSA) has been determined by cyclic voltammétrie measurements. The performances of Nafion membrane assemblies are higher than those obtained on reference assemblies, with gas diffusion layer supported electrodes. Promising results have been obtained on the assemblies performed for the first time with acid doped PBI membranes. The transfer process of the catalyst layer can also be used on other types of membrane.

Fuel cell technology has reached commercialisation of fuel cells in application areas such as residential power systems, automobile engines and driving of industrial manufacturing processes. This thesis gives an overview of the current state of fuel cell-based technology research and development, introduces a μCHP system sizing strategy and proposes methods of improving on the implementation of residential fuel cell-based μCHP technology. The three methods of controlling residential μCHP systems discussed in this thesis project are heat-led, electricity-led and cost-minimizing control. Simulations of a typical HT PEMFC -based residential μCHP unit are conducted using these control strategies. A model of a residential μCHP system is formulated upon which these simulated tests are conducted. From these simulations, equations to model the costs of running a fuel-cell based μCHP system are proposed. Having developed equations to quantify the running costs of the proposed μCHP system a method for determining the ideal size of a μCHP system is developed. A sizing technique based on industrial CHP sizing practices is developed in which the running costs and capital costs of the residential μCHP system are utilised to determine the optimal size of the system. Residential thermal and electrical load profile data of a typical Danish household are used. Having simulated the system a practical implementation of the power electronics interface between the fuel cell and household grid is done. Two topologies are proposed for the power electronics interface a three-stage topology and a two-stage topology. The efficiencies of the overall systems of both topologies are determined. The system is connected to the grid so the output of each system is phase-shifted and DC injection, harmonic distortion, voltage range and frequency range are determined for both systems to determine compliance with grid standards. Deviations between simulated results and experimental results are recorded and discussed and relevant conclusions are drawn from these.

This research is focused on the investigation of phase morphology and blend stability within ionomeric perfluorocyclobutane (PFCB)/poly(vinylidene difluoride) (PVDF) copolymer blend membranes. The morphologies of these unique materials, designed as proton exchange membranes (PEMs) for proton exchange membrane fuel cells (PEMFCs), have been examined not only in the as-cast/as-received state, but also as a function of exposure to various ex-situ aging environments. The morphological investigations used to probe the response of these ionomer blends have been designed to mimic the environment within a PEMFC and will therefore enhance our understanding of the implications of morphological changes which may occur during fuel cell operation. Thermal annealing of the membranes has been conducted to determine the materials' morphological response to various temperatures in the absence of hydration. The results of these thermal annealing studies have facilitated the isolation of morphological contributions stemming from thermal exposure. Immersion of the blend membranes in liquid water has allowed for singular identification of the role of hydration in the blend membranes' morphological rearrangement and phase stability. However, as the typical fuel cell environment to which these membranes will be exposed is complicated by the presence of both temperature and humidity, our ex-situ investigations have also included the exposure of PFCB/PVDF copolymer blend membranes to simultaneous thermal annealing and hydration conditions – a treatment we refer to as "hygrothermal aging." This unique procedure serves as a simplified method whereby the complex fuel cell environment may be simulated, and the resultant morphological response researched. While the work presented herein has enhanced our understanding of the blend stability of the specific membranes investigated, we have also advanced the fundamental knowledge of the role of morphology with respect to the fuel cell performance of blend materials and the corresponding implications of morphological rearrangements. Such an understanding is essential in the development of morphology-property relationships and eventual optimization of membrane materials designed for use in fuel cells. / Ph. D.

La pile à combustible convertit l’énergie chimique des réactants en énergie électrique continue, en chaleur et en eau. Elle est généralement utilisée autour d’un point de fonctionnement (ou zone) correspondant à un maximum de puissance électrique. Le courant continu produit par la réaction d’oxydo-réduction est proportionnel à la surface active de la pile et la tension, qui est d’environ 0,6 V au point de nominal de fonctionnement, peut être augmentée par la mise en série de plusieurs cellules (constituant un stack). En raison de son faible niveau de tension continue, son utilisation dans des systèmes électriques nécessitent de l’associer à des convertisseurs de puissance. Les travaux effectués dans le cadre de cette thèse s’intéressent au potentiel d’une source électrique continue basse tension et plus exactement à l’utilisation de la pile à combustible en fonctionnement source de courant commandée (par le débit d’un des réactants). L’expertise du laboratoire GREEN dans le domaine des supraconducteurs, nous a conduits naturellement vers une application innovante à savoir substituer les alimentations de puissance dédiées aux dispositifs supraconducteurs par une pile à combustible. Un premier essai prometteur mené sur une bobine supraconductrice de 4 mH a mis en évidence tout le potentiel d’une telle application et nous a encouragés à étendre l’étude à des bobines supraconductrices fortement inductives, des plusieurs henrys. En effet, les énergies mises en jeu sont alors plus importantes et exigent de dimensionner avec soin le banc d’essai, aussi bien du point de vue de la protection de la pile que des conditions opératoires. Pour ce faire, une modélisation et une expérimentation d’un ensemble pile à combustible/bobine supraconductrice ont également été réalisées. En parallèle du travail mené sur la partie alimentation de la bobine supraconductrice, nous avons travaillé sur le dimensionnement d’un dispositif supraconducteur innovant, communément appelé aimant vectoriel, à trois axes. Ce système peut servir comme charge pour une pile à combustible mais aussi, et surtout, comme outils de caractérisation d’échantillons supraconducteurs. Cet aimant vectoriel permet d’orienter dans les 3 directions de l’espace un champ magnétique de plusieurs teslas, uniforme à plus de 95 % dans une sphère de 100 mm de diamètre. Ce dimensionnement, nous a permis de concevoir et réaliser la structure supportant le bobinage du fil et de choisir un certain fil supraconducteur. Le système complet devant coûter moins de 50 k€, cryostat inclus, nous nous sommes orientés vers du fil supraconducteur à basse température critique, refroidi à l’hélium liquide / The fuel cell (FC) converts the chemical energy of the reactants into direct electrical energy, heat and water. The FC is generally used around an operating point (or area) corresponding to a maximum of electric power. The direct current produced by the redox reaction is proportional to the active surface of the single cell and its voltage, which is approximately 0.6 V at the nominal operating point, can be increase by connecting several cells in series (constituting a stack). Due to its low DC voltage amplitude, its use in electrical systems requires the use of power converters. In this work, we have been interested taking benefit of such DC low voltage power source and more precisely the use of the FC as a current source controllable by the one of the reactant flow rates. The expertise of GREEN laboratory in the field of superconductors has naturally led us to an innovative application, namely to substitute the power supplies dedicated to the superconducting devices by a FC. A first promising test conducted on a 4 mH superconducting coil highlighted the full potential of such an application and encouraged us to extend the study to highly inductive superconducting coils where the energies involved are more important. This requires to carefully design the test bench with a protection system for the FC as well as operating conditions. To this end, a FC model supplying a superconducting coil has been developed and tested experimentally. At the same time, we have focused on the supply part of the superconducting coil by designing an innovative superconducting device, commonly called a three-axis vector magnet. This system can be used as a load for a fuel cell, but also, and above all, as a tool for the characterization of superconducting samples. This vector magnet allows to orient a magnetic field of several tesla in the three space directions, with a uniformity of more than 95 % in a 100 mm sphere of diameter. This design allowed us to realize the windings supporting structure and to choose a superconducting wire. The complete system has to cost less than 50 k€, including the cryostat, we have finally choose a superconducting wire with low critical temperature, cooled by liquid helium

The subject of this thesis relates to the design of new polymer electrolytes for battery and fuel cell applications. Classical Molecular Dynamics (MD) modelling studies are reported of the nano-structure and the local structure and dynamics for two types of polymer electrolyte host: poly(ethylene oxide) (PEO) for lithium batteries and perfluorosulfonic acid (PFSA) for polymer-based fuel cells. Both polymers have been modified by side-chain substitution, and the effect of this on charge-carrier transport has been investigated. The PEO system contains a 89-343 EO-unit backbone with 3-15 EO-unit side-chains, separated by 5-50 EO backbone units, for LiPF6 salt concentrations corresponding to Li:EO ratios of 1:10 and 1:30; the PFSA systems correspond to commercial Nafion®, Hyflon® (Dow®) and Aciplex® fuel-cell membranes, where the major differences again lie in the side-chain lengths. The PEO mobility is clearly enhanced by the introduction of side-chains, but is decreased on insertion of Li salts; mobilities differ by a factor of 2-3. At the higher Li concentration, many short side-chains (3-5 EO-units) give the highest ion mobility, while the mobility was greatest for side-chain lengths of 7-9 EO units at the lower concentration. A picture emerges of optimal Li+-ion mobility correlating with an optimal number of Li+ ions in the vicinity of mobile polymer segments, yet not involved in significant cross-linkages within the polymer host. Mobility in the PFSA-systems is promoted by higher water content. The influence of different side-chain lengths on local structure was minor, with Hyflon® displaying a somewhat lower degree of phase separation than Nafion®. Furthermore, the velocities of the water molecules and hydronium ions increase steadily from the polymer backbone/water interface towards the centre of the proton-conducting water channels. Because of its shorter side-chain length, the number of hydronium ions in the water channels is ~50% higher in Hyflon® than in Nafion® beyond the sulphonate end-groups; their hydronium-ion velocities are also ~10% higher. MD simulation has thus been shown to be a valuable tool to achieve better understanding of how to promote charge-carrier transport in polymer electrolyte hosts. Side-chains are shown to play a fundamental rôle in promoting local dynamics and influencing the nano-structure of these materials.

The proton exchange membrane fuel cell (PEMFC) is a potential electrochemicalpower device for vehicles, auxiliary power units and small-scale power plants. In themembrane electrode assembly (MEA), which is the core of the PEMFC single cell,oxygen in air and hydrogen electrochemically react on separate sides of a membraneand electrical energy is generated. The main challenges of the technology are associatedwith cost and lifetime. To meet these demands, firstly, the component expensesought to be reduced. Secondly, enabling system operation at elevated temperatures,i.e. up to 120 °C, would decrease the complexity of the system and subsequentlyresult in decreased system cost. These aspects and the demand for sufficientlifetime are the strong motives for development of new materials in the field.In this thesis, MEAs based on alternative materials are investigatedwith focus on hydrocarbon proton-conducting polymers, i.e. ionomers, and newcatalyst supports. The materials are evaluated by electrochemical methods, such ascyclic voltammetry, polarisation and impedance measurements; morphological studiesare also undertaken. The choice of ionomers, used in the porous electrodes andmembrane, is crucial in the development of high-performing stable MEAs for dynamicoperating conditions. The MEAs are optimised in terms of electrode compositionand preparation, as these parameters influence the electrode structure andthus the MEA performance. The successfully developed MEAs, based on the hydrocarbonionomer sulfonated polysulfone (sPSU), show promising fuel cell performancein a wide temperature range. Yet, these membranes induce mass-transportlimitations in the electrodes, resulting in deteriorated MEA performance. Further,the structure of the hydrated membranes is examined by nuclear magnetic resonancecryoporometry, revealing a relation between water domain size distributionand mechanical stability of the sPSU membranes. The sPSU electrodes possessproperties similar to those of the Nafion electrode, resulting in high fuel cell performancewhen combined with a high-performing membrane. Also, new catalystsupports are investigated; composite electrodes, in which deposition of platinum(Pt) onto titanium dioxide reduces the direct contact between Pt and carbon, showpromising performance and ex-situ stability. Use of graphitised carbon as catalystsupport improves the electrode stability as revealed by a fuel cell degradation study.The thesis reveals the importance of a precise MEA developmentstrategy, involving a broad methodology for investigating new materials both as integratedMEAs and as separate components. As the MEA components and processesinteract, a holistic approach is required to enable successful design of newMEAs and ultimately development of high-performing low-cost PEMFC systems. / QC 20100922

In this thesis, a Proton Exchange Membrane Fuel Cell is modeled with COMSOL Multiphysics software. A cross-section that is perpendicular to the flow direction is modeled in a 2-D, steady-state, one-phase and isothermal configuration. Anode, cathode and membrane are used as subdomains and serpentine flow channels define the flow field . The flow velocity is defined at the catalyst layers as boundary conditions with respect to the current density that is obtained by using an agglomerate approach at the catalyst layer with the help of fundamental electrochemical equations. Darcy&rsquo / s Law is used for modeling the porous media flow. To investigate the effects of species depletion along the flow channels, a different type of cross-section that is parallel to the flow direction is modeled by adding flow channels as a subdomain to the anode and cathode. Differently, Brinkman Equations are used to define flow in the porous electrodes and the free flow in the channels is modeled with Navier-Stokes equations. By running parallel-to-flow model, mass fractions of species at three different locations (the inlet, the center and the exit of the channel) are predicted for different cell po- tentials. These mass fractions are used as inputs to the perpendicular-to-flow model to obtain performance curves. Finally, by maintaining restricted amount of species by having a very low pressure difference along the channel to represent a single mid-cell of a fuel cell stack, a species depletion problem is detected. If the cell potential is decreased beyond a critical value, this phenomenon causes dead places at which the reaction does not take place. Therefore, at these dead places the current density goes to zero unexpectedly.

Fuel cells are expected to play a major role in the economy of this century and for the foreseeable future. The use of hydrogen and fuel cells can address critical challenges in all energy sectors like commercial, residential, industrial, and transportation. Fuel cells are electrochemical devices that convert energy of a chemical reaction directly into electrical energy by combining hydrogen fuel with oxygen from air. If hydrogen is used as fuel, only byproducts are heat and water. The objective of this thesis is to investigate the effect of operating temperature and relative humidity (RH) of reactant gases on proton exchange membrane (PEM) fuel cell performance by adjusting the operation temperature of the fuel cell and humidification temperature of the reactant gases. In this study, the effect of the different operating parameters on the performance of single proton exchange membrane (PEM) fuel cell have been studied experimentally using pure hydrogen on the anode side and air on the cathode side. Experiments with different fuel cell operating temperatures, different air and hydrogen humidification temperatures have been carried out. The experimental results are presented in the form of polarization curves, which show the effects of the various operating parameters on the performance of the PEM fuel cell. The polarization curves data have been fit to a zero dimensional model, and the effect of the fuel cell operation and humidification temperatures on the kinetic parameters and the cell resistance have been determined. The fuel cell has been operated with 1.2 and 2 stoichiometry ratio for hydrogen and air, respectively. Fuel cell performance was detected at different fuel cell operation temperatures changing from 60 to 80 &ordm / C, and relative humidity of the entering gases changing from 20 to 100 % for air and 50 % and 100 % for hydrogen. Tests were performed in a PEM fuel cell test station. The highest performance of 275 mA/cm2 at 0.6 V and 650 mA/cm2 at 0.4 V was obtained for 50 % RH air with a constant 100 % relative humidity of hydrogen for working at atmospheric pressure and 60 oC fuel cell temperature. However, the highest performance of 230 mA/cm2 at 0.6 V for 50 % RH of air with a constant 100 % relative humidity of hydrogen and the highest performance of 530 mA/cm2 at 0.4 V for both 70 % RH and 100% RH air with a constant 100 % relative humidity of hydrogen was obtained for working at atmospheric pressure and 70 oC fuel cell temperature. Besides, the highest performance of 200 mA/cm2 at 0.6 V and 530 mA/cm2 at 0.4 V was obtained for 100 % RH air with a constant 100 % RH of hydrogen for working at atmospheric pressure and 80 oC fuel cell temperature.